U.S. patent number 3,927,080 [Application Number 05/502,706] was granted by the patent office on 1975-12-16 for process for producing n-phosphonomethyl glycine.
This patent grant is currently assigned to Monsanto Company. Invention is credited to Van R. Gaertner.
United States Patent |
3,927,080 |
Gaertner |
December 16, 1975 |
Process for producing N-phosphonomethyl glycine
Abstract
N-(phosphonomethyl)glycine is produced by the acid hydrolysis of
N-t-butyl-N-(phosphonomethyl)glycine or its esters.
N-(phosphonomethyl)glycine is useful as a post-emergent broad
spectrum herbicide.
Inventors: |
Gaertner; Van R. (Ballwin,
MO) |
Assignee: |
Monsanto Company (St. Louis,
MO)
|
Family
ID: |
26625864 |
Appl.
No.: |
05/502,706 |
Filed: |
September 3, 1974 |
Current U.S.
Class: |
562/17; 558/169;
560/155; 570/101; 987/168 |
Current CPC
Class: |
C07F
9/3813 (20130101) |
Current International
Class: |
C07F
9/00 (20060101); C07F 9/38 (20060101); C07F
009/38 () |
Field of
Search: |
;260/502.5 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Evans; Joseph E.
Attorney, Agent or Firm: Black; William T.
Claims
What is claimed is:
1. A process for producing N-(phosphonomethyl)glycine which
comprises forming an admixture of
N-t-butyl-N-(phosphonomethyl)glycine compound of the formula
##EQU3## wherein each R is individually hydrogen or an organic
group containing up to 18 carbon atoms, with an aqueous hydrohalic
acid consisting of hydrochloric, hydrobromic or hydriodic, the
concentration of said aqueous hydrohalic acid being at least 20% by
weight and heating said admixture to a temperature sufficiently
elevated so as to remove said t-butyl group.
2. A process as claimed in claim 1 wherein the temperature is from
100.degree. to 130.degree.C.
3. A process as claimed in claim 2 wherein R is a lower alkyl
ester.
4. A process as claimed in claim 3 wherein the aqueous hydrohalic
acid is hydrobromic acid.
5. A process as claimed in claim 4 wherein the temperature is from
100.degree. to 130.degree.C.
6. A process as claimed in claim 5 wherein
N-t-butyl-N-(phosphonomethyl)glycine compound is triethyl
N-t-butyl-N-(phosphonomethyl)glycinate.
Description
This invention relates to a process for producing
N-(phosphonomethyl)glycine by the acid catalyzed hydrolysis of
N-t-butyl-N-(phosphonomethyl)glycine or its esters.
It is known that N-(phosphonomethyl)glycine can be produced by the
strong acid catalyzed decomposition of
N-(phosphonomethyl)iminodiacetic acid and also by the acid
hydrolysis of N-benzyl-N-(phosphonomethyl)glycine esters.
It has now been discovered that N-(phosphonomethyl)glycine can be
produced by the hydrolysis of N-t-butyl-N-(phosphonomethyl)glycine
or its esters with aqueous hydrohalic acid such as hydrochloric
acid, hydrobromic acid and hydriodic acid. This reaction is easily
conducted and the N-(phosphonomethyl)-glycine produced is of
greater than 90% purity inasmuch as the products of the hydrolysis
are volatile and easily removed leaving the
N-(phosphonomethyl)glycine as a residue.
It is believed that the reaction takes place in accordance with the
following equation which, for convenience, shows the acid
hydrolysis-decomposition of triethyl
N-t-butyl-N-(phosphonomethyl)glycinate ##EQU1##
In accordance with the process of this invention,
N-(phosphonomethyl)glycine is produced by the acid hydrolysis of an
N-tertiary butyl-N-(phosphonomethyl)glycine compound of the formula
##EQU2## wherein each R is individually hydrogen or an organic
group containing from 1 to 18 carbon atoms. Preferably the R's are
organic groups containing up to 8 carbon atoms and even more
preferably lower alkyl groups.
More particularly, the process of this invention is conducted by
forming an admixture of an N-t-butyl-N-(phosphonomethyl)glycine
compound of formula (I) with an aqueous hydrohalic acid and heating
said admixture to a temperature sufficiently elevated to initiate
and sustain the hydrolysis-decomposition reaction.
In conducting the process of this invention, one can employ aqueous
hydrohalic acids such as hydrochloric, hydrobromic and hydriodic.
It is preferred in conducting the process of this invention that
the aqueous hydrohalic acid be at least 20% by weight. It is even
more preferred to employ the aqueous hydrohalic acid at
concentrations of at least 30% by weight. Although at lower
concentration the reaction would take place, the reaction time
would be greatly extended and the yields of
N-(phosphonomethyl)glycine would be low.
In conducting the process of this invention, the temperature of
reaction can range from as low as 90.degree. to 150.degree.C. or
even higher. It is preferred for ease of reaction and to obtain the
best yield of product to conduct the process of this invention from
about 110.degree. to about 130.degree.C., preferably up to the
reflux temperature of the particular aqueous hydrohalic acid being
employed.
The time of reaction is not narrowly critical and can vary from as
low as 1 minute contact time to as high as 40 or more hours. Of
course, it is obvious to those skilled in the art that yield of
product will vary with the reaction time and the temperature of the
reaction. For example, shorter reaction times can be employed when
the higher reaction temperatures are employed and longer reaction
times will be employed at the lower range of temperature.
The ratio of the hydrohalic acid to the
N-t-butyl-N-(phosphonomethyl)glycinate can range from one mole
N-t-butyl-N-(phosphonomethyl)glycinate to 100 equivalents acid to 1
part N-t-butyl-N-(phosphonomethyl)glycinate to three equivalents
acid. However, for ease of reaction and recovery and economics, it
is preferred to employ the N-t-butyl-N-(phosphonomethyl)-glycinate
in amounts of from one mole to 10 to 15 equivalents of the
hydrohalic acid.
The process of the instant invention is usually conducted at
atmospheric pressure for ease of reaction and economics. Higher and
lower pressures can be employed if proper venting techniques are
employed to allow the escape of the volatile by-products.
The starting materials employed in the process of this invention
are prepared by the following general procedure.
The alkyl N-t-butylglycine ester may be prepared from t-butylamine
and alkyl bromoacetates. Thus, 16.7 g (0.1 mole) of ethyl
bromoacetate was added dropwise to 21.9 g. (0.3 mole) t-butylamine,
stirred and cooled at 5.degree.-10.degree.C. A solid precipitated
and after stirred 3 hours at 0.degree.-10.degree.C., the mixture
was treated with ether and 0.1 mole of 50% aqueous sodium hydroxide
solution. The ether layer was separated, dried over
anhydromagnesium sulfate, filtered and concentrated. The residual
oil was distilled at 85.degree.-100.degree.C./0.3 mm, to give 9.4
g. (58%) of ethyl N-t-butyl-glycinate.
A cooled (10.degree.C.) solution of stable amino acid ester in
ethanol, is treated with commercial 36-37% formalin, using 0.1 mole
of formaldehyde equivalent for 0.1 mole of amino group content. The
addition is slightly exothermic and cooling may be necessary to
maintain the mixture at 25.degree.-35.degree.C. To the resulting
solution, after stirring about 15 minutes, is added 0.11 mole of
the diorgano phosphite at once, cooling below 50.degree.C. if
necessary.
The mixture is heated to reflux and then toluene added to remove
the alcohol and water by azeotropic distillation. A final period of
1 hour at 115.degree.C. completes the reaction.
The toluene solution is decanted or filtered to remove insoluble
salts, then concentrated on a rotary evaporator, finally at
100.degree./1 mm. or less, to remove unconverted phosphite.
The residual oil is again filtered, if necessary, and distilled in
a molecular still, such as a wiped-wall still which minimizes
thermal decomposition of labile compounds of low volatility, at
high vacuum, in the range of 1-20 microns or at the minimum
temperature which will strip the product from less volative,
resinous by-products. Triethyl
N-t-butyl-N-(phosphonomethyl)glycinate was prepared in the above
manner; it was distilled in a short-path still at
121.degree.-125.degree.C./0.2 mm.
Anal. Calc'd for: C.sub.13 H.sub.28 NO.sub.5 P: C: 50.4; H: 9.12;
P: 10.02 Found: C: 50.36; H: 8.95; P: 10.36
The following example serves to further illustrate the invention.
All parts are parts by weight unless otherwise expressly set
forth.
EXAMPLE 1
A solution of 5.0 g. of N-t-butyl-N-(phosphonomethyl)glycinate in
20 ml. of 48% aqueous hydrobromic acid was changed into a suitable
reactor and heated to reflux for 3 hours at 120.degree.C., allowing
ethyl bromide and isobutylene to escape through the condenser. The
solution was concentrated on the vacuum rotary evaporator to remove
most of the excess hydrobromic acid and crystals separated. The
slurry was triturated twice with ether, which was decanted, then
diluted with ethanol, filtered and rinsed with aqueous ethanol and
dried. The white crystals 3.2 g., (95%), were identified as pure
N-(phosphonomethyl)glycine by the NMR spectrum in D.sub.2 O and by
analysis.
Anal. Calc'd for C.sub.3 H.sub.8 NO.sub.5 P: C: 21.3; H: 4.77; P:
18.3 Found: C: 20.2; H: 4.80; P: 18.48
* * * * *